CN202107686U - Oil-water precipitation separation device - Google Patents
Oil-water precipitation separation device Download PDFInfo
- Publication number
- CN202107686U CN202107686U CN2011201923275U CN201120192327U CN202107686U CN 202107686 U CN202107686 U CN 202107686U CN 2011201923275 U CN2011201923275 U CN 2011201923275U CN 201120192327 U CN201120192327 U CN 201120192327U CN 202107686 U CN202107686 U CN 202107686U
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- CN
- China
- Prior art keywords
- separating tank
- grease
- outlet
- steam
- coil pipe
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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Abstract
The utility model discloses an oil-water precipitation separation device, which comprises a separation tank, wherein the separation tank comprises a cylindrical upper part and a tapered lower part, and an oil grease outlet, an oil grease inlet, a steam inlet, a steam outlet and a coil pipe are arranged on the separation tank; and the steam inlet is connected with the steam outlet by the coil pipe, and a water outlet is arranged at the bottom of the separation tank. The oil-water precipitation separation device has the advantages that: the coil pipe is arranged in the sealed container tank, and circulating steam is introduced into the coil pipe, so that the high temperature of steam is used for dewatering oil grease, and thus the dewatering efficiency is improved.
Description
Technical field
The utility model relates to a kind of biofuel processing units, and specifically a kind of profit precipitation separation device belongs to the biofuel manufacture field.
Background technology
Biofuel (biodiesel fuel) is raw material with the animal-plant oil, under catalyst action, exchanges the diesel oil processed through fat with methyl alcohol or ethanol.Usually with the reproducibility diesel oil fuel of waterplant grease such as oil crops, wild oilseed plant and engineering microalgae and animal oil and fat, food garbage wet goods the replaced petrifaction diesel that to be raw oil process through ester exchange process.
The production technology of chemical process, physics method and biological enzyme is adopted in the manufacturing of biofuel at present usually.Usually after need carrying out the esterification processing to animal oil and fat, food garbage wet goods raw material; Need the product of reaction be washed; Remove the impurity of dereaction, carry out precipitated and separated after the washing, grease and water sepn; Yet do not have the complete profit precipitation separation device of a cover at present, caused the reduction of production efficiency.
The utility model content
In order to address the above problem; The utility model has designed a kind of profit precipitation separation device, and this equipment is through being provided with coil pipe, logical cyclic steam in the coil pipe in airtight container tank; Temperature through steam promotes deposition; With grease and water stratification, the water port draining that the water of lower floor is provided with through the bottom, of the transition pipeline sucking-off of remaining grease through being provided with.
The technical scheme of the utility model is:
A kind of profit precipitation separation device comprises separating tank, and described separating tank divides two portions up and down, and top is round shape, and the bottom is conical;
Described separating tank is provided with grease outlet and grease import, and transition pipeline enters into the bottom of separating tank through the grease outlet;
Described separating tank is provided with steam inlet and vapour outlet, is provided with coil pipe in the described separating tank, and described coil pipe connects described steam inlet and vapour outlet;
The bottom of described separating tank is provided with water port.
Further, described steam outlet is provided with drain valve.
Grease enters in the separating tank through the grease import; Steam enters into coil pipe through steam inlet, flow out from vapour outlet then, with this to the greasy heating in the separating tank; Temperature through steam promotes deposition; With grease and water stratification, the water port draining that the water of lower floor is provided with through the bottom, of the transition pipeline sucking-off of remaining grease through being provided with.
The advantage of the utility model is: this equipment is through being provided with coil pipe in airtight container tank, logical cyclic steam is realized greasy dehydration through the high temperature of steam in the coil pipe, has improved dewatering efficiency.
The utility model is described further with implementing below in conjunction with accompanying drawing.
Description of drawings
Fig. 1 is the structural representation of a kind of profit precipitation separation device of the utility model embodiment;
Among the figure: 1-separating tank, 2-transition pipeline, the outlet of 3-grease, 4-steam inlet, 5-water port, the import of 6-grease, 7-vapour outlet, 8-drain valve, 9-coil pipe.
Embodiment
Below the preferred embodiment of the utility model is described, should be appreciated that preferred embodiment described herein only is used for explanation and explains the utility model, and be not used in qualification the utility model.
Embodiment 1
As shown in Figure 1, a kind of profit precipitation separation device comprises separating tank 1, and described separating tank is two portions about in the of 1 minute, and top is round shape, and the bottom is conical; Described separating tank 1 is provided with grease outlet 3 and grease import 6, and transition pipeline 2 enters into the bottom of separating tank 1 through grease outlet 3; Described separating tank 1 is provided with steam inlet 4 and vapour outlet 7, is provided with coil pipe 9 in the described separating tank 1, and described coil pipe 9 connects described steam inlet 4 and vapour outlet 7; Described vapour outlet 7 places are provided with drain valve 8; The bottom of described separating tank 1 is provided with water port 5.
Grease enters in the separating tank 1 through grease import 3; Steam enters into coil pipe 9 through steam inlet 6, flow out from vapour outlet 7 then, with this to the greasy heating in the separating tank 1; Temperature through steam promotes deposition; With grease and water stratification, water port 5 drainings that the water of lower floor is provided with through the bottom, of transition pipeline 2 sucking-offs of remaining grease through being provided with.
What should explain at last is: the above is merely the preferred embodiment of the utility model; Be not limited to the utility model; Although the utility model has been carried out detailed explanation with reference to previous embodiment; For a person skilled in the art, it still can be made amendment to the technical scheme that aforementioned each embodiment put down in writing, and perhaps part technical characterictic wherein is equal to replacement.All within the spirit and principle of the utility model, any modification of being done, be equal to replacement, improvement etc., all should be included within the protection domain of the utility model.
Claims (2)
1. profit precipitation separation device is characterized in that: comprise separating tank, described separating tank divides two portions up and down, and top is round shape, and the bottom be a taper shape;
Described separating tank is provided with grease outlet and grease import, and transition pipeline enters into the bottom of separating tank through the grease outlet;
Described separating tank is provided with steam inlet and vapour outlet, is provided with coil pipe in the described separating tank, and described coil pipe connects described steam inlet and vapour outlet;
The bottom of described separating tank is provided with water port.
2. a kind of grease dehydration equipment according to claim 1, it is characterized in that: described steam outlet is provided with drain valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201923275U CN202107686U (en) | 2011-06-09 | 2011-06-09 | Oil-water precipitation separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201923275U CN202107686U (en) | 2011-06-09 | 2011-06-09 | Oil-water precipitation separation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202107686U true CN202107686U (en) | 2012-01-11 |
Family
ID=45433129
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201923275U Expired - Fee Related CN202107686U (en) | 2011-06-09 | 2011-06-09 | Oil-water precipitation separation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202107686U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104479863A (en) * | 2014-12-11 | 2015-04-01 | 平顶山市亿鑫达生物能源有限公司 | Device and method for pre-treating raw oil for production of biodiesel |
-
2011
- 2011-06-09 CN CN2011201923275U patent/CN202107686U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104479863A (en) * | 2014-12-11 | 2015-04-01 | 平顶山市亿鑫达生物能源有限公司 | Device and method for pre-treating raw oil for production of biodiesel |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120111 Termination date: 20140609 |